Method of making a composite nuclear fuel material consisting of dispersed (u,pu)o2 aggregates

ABSTRACT

The invention relates to a production process of a composite material composed of aggregates of a blend of UO 2  and of PuO 2  dispersed in a UO 2  matrix comprising the steps of dry co-grinding of a UO 2  powder and of a PuO 2  powder in order to obtain a homogenous primary blend, of consolidating the primary blend in order to obtain cohesive aggregates, of sieving the aggregates in a range of 20 to 350 μm, of diluting the sieved aggregates in a UO 2  matrix in order to obtain a powder blend, of pelletising the powder blend and of sintering the pellets obtained in order to obtain the composite.

FIELD OF THE INVENTION

[0001] This invention relates to a production process of a composite nuclear fuel material composed of aggregates of a ground powder blend of UO₂ and PuO₂ dispersed in a UO₂ matrix preferably depleted in ²³⁵U.

[0002] The composite in question possesses after sintering a microstructure of ceramic-ceramic (CERCER) type in the form of relatively spherical calibrated aggregates of solid solution (U,Pu)O₂ dispersed in the UO₂ matrix.

[0003] This is a nuclear fuel material with improved fission gas release properties.

BRIEF DESCRIPTION OF THE BACKGROUND ART

[0004] MOX (Mixed Oxide) fuel is at present produced industrially using a process known as MIMAS (MIcronized MASter blend). This process comprises successively a step of grinding oxides of uranium and plutonium, a step of diluting the powders obtained (primary blend) in the uranium oxide (UO₂) and a step of sintering.

[0005] The MOX fuel produced by this process has a two-phase structure, one phase (U,Pu)O₂ composed of solid solutions with a Pu/U+Pu content that can vary in the range of 30 to 5% of Pu and a UO₂ phase. The (U,Pu)O₂ phase exists either in aggregate form or in the form of “filaments” forming a continuous network in the fuel.

[0006] On irradiation, the fission gases are essentially created in the plutonium-bearing zones and install themselves over short distances (7 to 9 μm) then diffuse through the UO₂ matrix before being released outside the fuel.

[0007] An improvement of the material consists in exacerbating the biphasic character of the present fuel to tend towards a material that isolates the plutonium-bearing zones in a UO₂ matrix, which is intended to act as a retention barrier to the fission gases.

SUMMARY OF THE INVENTION

[0008] The precise object of the present invention is to provide a production process for a composite material consisting of cohesive aggregates of a ground powder blend of UO₂ and of PuO₂ dispersed in a UO₂ matrix that makes it possible to obtain a material capable of limiting fission gas release.

[0009] The cohesive aggregates are obtained, according to the invention, either by mechanical granulation, or by calcinating the primary blend of UO₂ and PuO₂.

[0010] The process of the present invention includes the following steps:

[0011] dry co-grinding a UO₂ powder and a PuO₂ powder so as to obtain a homogenous primary blend,

[0012] consolidating the primary blend so as to obtain cohesive aggregates of the blend of UO₂ and of PuO₂,

[0013] sieving the aggregates between 20 and 350 μm,

[0014] diluting the sieved aggregates in a UO₂ matrix so as to obtain a powder blend,

[0015] pelletising the powder blend, and

[0016] sintering the pellets obtained in order to obtain the composite.

[0017] The process of the present invention makes it possible to isolate the fissile matter comprising the plutonium-bearing aggregates of calibrated ground powders of UO₂ and of PuO₂ and to distribute them homogenously through the fertile matrix composed of UO₂.

[0018] Appended FIGS. 2a), 2 b) and 3 represent three photographs of microstructures of sintered composite materials composed of precalcinated or granulated aggregates (marker 1) of (U,Pu) O₂ dispersed in a UO₂ matrix (marker 2).

[0019] According to the invention, the primary blend of UO₂ and of PuO₂ is comprised preferably of a UO₂ content in the range of 60 to 90 wt. % and of a PuO₂ content in the range of 40 to 10 wt. % of the total mass of the blend, preferably 75 wt. % of UO₂ and 25 wt. % of PuO₂. The mass of PuO₂ can be totally or partially replaced by discarded manufactured powders comprised of mixed oxides (U,Pu) O₂.

[0020] According to a first embodiment of the present invention, the step of consolidation to obtain cohesive aggregates can include the following steps:

[0021] compacting the homogenous primary blend at a pressure in the range of 150 to 600 MPa in order to obtain a blank,

[0022] crushing the blank obtained in order to obtain granules, and

[0023] spheroidising the granules.

[0024] This first embodiment of the present invention comprises mechanically granulating the primary blend compacts. This consolidation brings about sufficient cohesion of aggregates to withstand without deterioration the subsequent steps of diluting and pelletising of the process of the present invention. The blend can be compacted by using a single or double effect uniaxial press. This is preferably carried out at a pressure of 300 MPa. The crushing can be carried out using any known appropriate means, for example using an industrial crusher. The granules can for example be spheroidised using simple self-abrasion of the crushed products, for example in a mixer of the TURBULA (registered trademark) type (oscillo-rotary mixer-shaker).

[0025] According to a second embodiment of the present invention, the consolidation of a primary blend can be carried out using a heat treatment calcinating the primary blend at a temperature of 1000 to 1400° C., preferably at a temperature of 1000° C. The consolidated primary blend is the mixture of UO₂ and of PuO₂ produced by co-grinding. Calcination gives the primary blend a sufficient degree of cohesion for it to withstand without deterioration the subsequent steps of dilution and pelletising of the process of the present invention while preserving high sphericity. Preferably, the heat treatment is carried out in an humidified or non-humidified atmosphere of 95 vol. % argon and 5 vol. % hydrogen. When the heat treatment atmosphere is humidified, it is preferably humidified with a partial pressure ratio P_(H2)/P_(H20) in the range of 50 to 20.

[0026] The sieving can be carried out using a stainless steel sieve with mesh size in the range of 20 to 350 μm, preferably in the range of 125 to 350 μm. Thus the cohesive aggregates can have a dimension (diameter) in the range of 20 to 350 μm, preferably in the range of 125 to 350 μm.

[0027] The dilution of the aggregates in the UO₂ matrix can be carried out for example by mechanical stirring. This should preferably not break the aggregates. The aggregates can be diluted in the UO₂ matrix at a concentration of 20 to 35 vol. % of the total volume of the green blend obtained, preferably at a concentration of 20 vol. % of the total volume of the green blend. These quantities yield a composite material advantageously containing between 2.1 and 9.45% of plutonium oxide.

[0028] According to the invention, pelletising can be carried out using a uniaxial hydraulic press, for example at a pressure of 500 MPa.

[0029] According to the invention, the sintering step can be carried out a temperature of approximately 1700° C. It can be carried out in a sintering furnace by following a thermal cycle comprising the following successive steps of:

[0030] raising the temperature at 200° C./hour,

[0031] plateauing at approximately 1700° C., and

[0032] cooling at approximately 400° C./hour down to 1000° C., then by following furnace inertia.

[0033] The sintering step is preferably carried out in an humidified or non-humidified atmosphere of 95 vol. % argon and 5 vol. % hydrogen. When the sintering atmosphere is humidified, it is preferably humidified with a partial pressure ratio P_(H2)/P_(H20) in the range of 50 to 20.

[0034] Other characteristics and advantages will become obvious on reading the following examples, which are, of course, given to illustrate the invention and not to limit it as refers to the appended drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

[0035]FIG. 1 represents a flow chart of the sequence of the different steps of the production process of a composite according to the process of the present invention.

[0036]FIG. 2a) is a photograph of a microstructure obtained by the mechanical granulation process of the present invention at a magnification of ×20, after 4 hours of sintering at 1700° C. in a non-humidified 95% Ar-5% H₂ atmosphere, of a CERCER composite containing 20 vol. % of aggregate 75% UO₂-25% PuO₂ granulated after compaction at 300 MPa (image obtained by optical microscopy); and

[0037]FIG. 2b) is a photograph of the material represented in FIG. 2a) at a magnification of ×200, and

[0038]FIG. 3 represents a photograph of a microstructure of a composite material consisting of a solid solution (U,Pu)O₂ dispersed in a UO₂ matrix, at a concentration of 20 vol. % of aggregates consolidated by a heat treatment at 1000° C., according to the process of the present invention.

EXAMPLES

[0039] The sequence of the different steps of the manufacturing process of sintered composites consisting of aggregates of solid solution of (U,Pu)O₂ dispersed in a UO₂ matrix according to the process of the present invention is indicated in the flow chart in FIG. 1.

Example 1 Dry Co-grinding of UO₂ and PuO₂ Powders

[0040] Different homogenous matrix blends of powders of uranium and plutonium dioxides produced by processes known to prior art have been produced with proportions of powders in the ranges of 60 to 90 wt. % of UO₂ and of 40 to 10 wt % of PuO₂ compared to the total mass of the blend.

[0041] These blends were produced by dry co-grinding the rough powders, in a jar rotating at 48 r.p.m. for 6 hours. The grinding media were uranium metal balls. No organic, pore-forming or lubricant additives were used.

Example 2 Consolidation of the Primary Blend by Mechanical Granulation

[0042] This example illustrates a first embodiment of the consolidation step of the aggregates of the process of the present invention.

[0043] One of the matrix blends at 25 vol. % of PuO₂ obtained in example 1 was compacted in different tests at different granulation pressures in a range of 0 (non-compacted powder from co-grinding) to 600 MPa, using a single effect uniaxial press.

[0044] The blanks thus obtained were then crushed manually in an agate mortar, and the crushed products obtained were spheroidised by self-abrasion by a Pyrex (commercial brand) round bottom flask inserted in a grinding jar rotating at 48 r.p.m. for one and a half hours.

Example 3 Consolidation of the Primary Blend by Heat Treatment

[0045] This example illustrates a second embodiment of the consolidation step of the aggregates of the process of the present invention.

[0046] The heat treatment was applied to one of the matrix blends at 25 vol. % of PuO₂ obtained in example 1, in a flow of a non-humidified 95% Ar-5% H₂ mixture.

[0047] The thermal cycle used corresponded to a rise in temperature at 200° C./hour to a temperature of 1000, 1200 or 1400° C. followed, with no plateau, by cooling at 400° C./hour to ambient temperature.

[0048] This consolidation treatment produced consolidated aggregates of high sphericity, for each blend of UO₂ and of PuO₂.

Example 4 Sieving the Aggregates

[0049] The aggregates obtained in examples 2 and 3 were sieved using a stainless steel sieve with mesh size in the range of 125 to 250 μm.

Example 5 Diluting the Sieved Aggregates in the UO₂ Matrix

[0050] After mechanical granulation or thermal consolidation, the plutonium-bearing aggregates were mixed with UO₂ powder for 1 hour 30 minutes in a round bottom flask placed on the driving rolls of a grinder and turning at a speed of 46 r.p.m.

Example 6 Pelletising the Green Blend

[0051] Shaping the composites by pelletising was done using a single effect uniaxial press, operating at a pressure of 500 MPa. A pellet of zinc stearate was pressed regularly after producing two cylinders of composite, in order to ensure the lubrication of the press matrix. The samples obtained took the form of cylinders of approximately 7 mm in diameter and 9 mm in height.

Example 7 Sintering the Pellets Obtained in Example 6 in Order to Form the Composite

[0052] The samples placed in a sintering box were sintered in a Degussa (commercial brand) bell furnace. The thermal cycle used was as follows:

[0053] raising the temperature at 200° C./hour;

[0054] 4 hours of plateau at 1700° C.;

[0055] cooling at 400° C./hour down to 1000° C., then by following switched off furnace inertia until ambient temperature was reached.

[0056] The different composites were sintered in a reducing atmosphere consisting of a flow of a non-humidified mixture of 95% argon and 5% hydrogen. A level of residual humidity of approximately 100 ppm was measured in the gas at furnace exit, at ambient temperature. This corresponds to an oxygen potential, ΔG°, at 1700° C. of −478 kJ/moleO₂.

[0057] The characteristics of the UO₂—PuO₂ aggregates used and of the CERCER composites obtained are presented in the following table 1. TABLE 1 CHARACTERISTICS OF AGGREGATES CHARACTERISTICS Green Green Sintered Granulation Calcination Apparent Aggregate Apparent Apparent Test Wt. % of pressure Temperature Density Fractional Wt. % of Density Density n° PuO₂ (MPa) (° C.) (g/cm³) Volume PuO₂ (g/cm³) (g/cm³) Granulation 1 10 300 nil 6.8 20.2 2.1 6.5 10.5 2 25 300 nil 6.9 19.9 5.3 6.5 10.5 3 40 300 nil 7.0 20.5 8.6 6.5 10.5 4 25 600 nil 7.3 25.6 7.35 6.5 10.5 5 25 300 nil 6.9 35.7 9.45 6.6 10.5 Reference 6 25 nil nil 5.4 25.0 5.2 6.6 10.5 Example Heat 7 25 nil 1000 7.3 18.5 4.9 6.5 10.5 Treatment 8 25 nil 1200 8.0 20.2 5.6 6.5 10.5 9 25 nil 1400 9.6 20.1 6.2 6.6 10.2

[0058] The products obtained after sintering have a microstructure of the type of those presented in FIGS. 2a), 2 b) and 3. The relatively regular distribution of the plutonium-bearing aggregates (white spots on the photographs) in the matrix show that the process of the present invention of product preparation meets the objective for obtaining a composite of individualized aggregates enclosing the totality of the mixed oxide. In view of the dilution process chosen, as described in example 5 above, the composite presenting the required qualities can only be obtained if the plutonium-bearing aggregates (UO₂—PuO₂) used are cohesive enough to preserve their integrity during this step of the process.

[0059] The results obtained have shown that the aggregates prepared according to the present invention by mechanical granulation or thermally consolidated at 1000° C. present the properties required for the production of the composites. 

1. Process for producing a composite material consisting of aggregates of a blend of ground UO₂ and PuO₂ powders dispersed in a UO₂ matrix, comprising the following steps of: (a) dry co-grinding a UO₂ powder and a PuO₂ powder so as to obtain a homogenous primary blend, (b) consolidating the primary blend so as to obtain cohesive aggregates of the UO₂—PuO₂ blend, (c) sieving the aggregates between 20 and 350 μm, (d) diluting the sieved aggregates in a UO₂ matrix so as to obtain a powder blend, (e) pelletising the powder blend, and (f) sintering the pellets obtained in order to obtain the composite.
 2. Process of claim 1, wherein the blend consolidation step in order to obtain cohesive aggregates comprises the following steps of: (a) compacting the homogenous primary blend at a pressure in the range of 150 to 600 MPa in order to obtain a blank, (b) crushing the blank obtained in order to obtain granules, and (c spheroidising the granules.
 3. Process of claim 2, wherein the compaction of the blend is carried out at a pressure of 300 MPa.
 4. Process of claim 1, wherein the consolidation of the primary blend in order to obtain cohesive aggregates is carried out using heat treatment of the primary blend at a temperature of 1000 to 1400° C.
 5. Process of claim 4, wherein the consolidation of the primary blend in order to obtain cohesive aggregates is carried out using heat treatment of the primary blend at a temperature of 1000° C.
 6. Process of claim 4, wherein consolidation heat treatment is carried out in a humidified or non-humidified atmosphere of 95 vol. % argon and 5 vol. % hydrogen.
 7. Process of claim 1, wherein the size of the sieved cohesive aggregates ranges between 20 and 350 μm.
 8. Process of claim 1, wherein the PuO₂ powder is totally or partially replaced by a discarded manufactured powder comprised of mixed oxides (U,Pu)O_(2.)
 9. Process of claim 1, wherein the primary blend of UO₂ and of PuO₂ is comprised of 60 to 90 wt. % UO₂ and 40 to 10 wt. % PuO₂ relative to the total mass of the blend.
 10. Process of claim 1, wherein the primary blend of UO₂ and PuO₂ is comprised of 75 wt. % UO₂ and 25 wt. % PuO₂ relative to the total mass of the blend.
 11. Process of claim 1, wherein the sieved cohesive aggregates are diluted in the UO₂ matrix at a concentration of 20 to 35 vol. % relative to the total volume of the powder blend obtained.
 12. Process of claim 1, wherein the sieved cohesive aggregates are diluted in the UO₂ matrix at a concentration of 20 vol. % relative to the total volume of the powder blend.
 13. Process of claim 1, wherein the pelletising step is carried out using a uniaxial hydraulic press.
 14. Process of claim 1, wherein the sintering step is carried out at a temperature of approximately 1700° C.
 15. Process of claim 1, wherein the sintering step is carried out in a furnace following a thermal cycle comprising the following successive steps of: (a) raising the temperature at 200° C./hour, (b) stabilizing at approximately 1700° C., and (c) cooling at approximately 400° C./hour down to 1000° C., then by following furnace inertia, wherein the sintering step is preferably carried out in a humidified or non-humidified atmosphere of 95 vol. % argon and 5 vol. % hydrogen.
 16. Process of claim 5, wherein consolidation heat treatment is carried out in a humidified or non-humidified atmosphere of 95 vol. % argon and 5 vol. % hydrogen. 